Classifications

• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
  • C11D1/66—Non-ionic compounds
  • C11D1/72—Ethers of polyoxyalkylene glycols
  • C11D1/721—End blocked ethers
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/02—Preparation of ethers from oxiranes
  • C07C41/03—Preparation of ethers from oxiranes by reaction of oxirane rings with hydroxy groups
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
  • C07C41/01—Preparation of ethers
  • C07C41/05—Preparation of ethers by addition of compounds to unsaturated compounds
  • C07C41/06—Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C43/00—Ethers; Compounds having groups, groups or groups
  • C07C43/02—Ethers
  • C07C43/03—Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
  • C07C43/04—Saturated ethers
  • C07C43/10—Saturated ethers of polyhydroxy compounds
  • C07C43/11—Polyethers containing —O—(C—C—O—)n units with ≤ 2 n≤ 10
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C43/00—Ethers; Compounds having groups, groups or groups
  • C07C43/02—Ethers
  • C07C43/20—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring
  • C07C43/205—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring the aromatic ring being a non-condensed ring
  • C07C43/2055—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring the aromatic ring being a non-condensed ring containing more than one ether bond
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C43/00—Ethers; Compounds having groups, groups or groups
  • C07C43/02—Ethers
  • C07C43/20—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring
  • C07C43/23—Ethers having an ether-oxygen atom bound to a carbon atom of a six-membered aromatic ring containing hydroxy or O-metal groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
  • C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
  • C08G65/32—Polymers modified by chemical after-treatment
  • C08G65/329—Polymers modified by chemical after-treatment with organic compounds
  • C08G65/337—Polymers modified by chemical after-treatment with organic compounds containing other elements
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
  • C07C2602/00—Systems containing two condensed rings
  • C07C2602/36—Systems containing two condensed rings the rings having more than two atoms in common
  • C07C2602/42—Systems containing two condensed rings the rings having more than two atoms in common the bicyclo ring system containing seven carbon atoms
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S516/00—Colloid systems and wetting agents; subcombinations thereof; processes of
  • Y10S516/01—Wetting, emulsifying, dispersing, or stabilizing agents

Definitions

• R is an n-alkyl, branched alkyl or alkyl-phenyl group, and R is a tert.-alkyl group or alicyclic hydrocarbon radical.
• compositions are prepared by mixing together compounds of the type RO(CH CH O) OH with tertiary olefins having from four to twelve carbon atoms, and then contacting the mixture with an anhydrous macroreticular resinous polysulfonic acid at temperatures ranging from about 0 to 70 C. and at atmospheric or autogenous pressure. After the reactants have been in contact with the catalyst for a sufficient length of time to obtain the desired degree of etherification, the catalyst is removed. Any traces of acidic materials leached out of the catalyst are neutralized by the addition of a base. Any unreacted olefin is then separated by distillation or solvent extraction, leaving the product and any unreacted starting alcohol. The product may be further purified by solvent extraction or other means to remove unreacted starting alcohol.
• the principal and preferred products of this invention are the t-butyl ethers of octylphenoxypolyethoxyethanols having an average of about 9 to 13 oxyethylene units, and the camphene ethers of octylphenoxyethanols having an average of about 25 to 35 oxyethylene units.
• Both of these types of products are characterized by their high resistance to oxidative degradation when formulated with strongly alkaline materials like solid NaOH or KOH. They are also low foaming compounds which have an excellent defoaming action, and they are therefore highly useful in such applications as mechanical dishwashers and metal cleaning operations.
• the compounds likewise have utility as Wetting agents and detergents in textile processing, and also as detergents for cleaning non-porous surfaces. Their general usefulness as non-ionic surface- 3,281,475 Patented Oct. 25, 1966 active agents is not impaired by the presence of the t-alkyl or terpenyl groups.
• the method of preparing these products utilizes the termination reaction of nonionics, i.e. removal of the terminal hydroxyl group by conversion to an ether linkage. Most termination reactions are diflicult to make go to completion as they are carried out by the well-known Williamson synthesis method, i.e. reaction of the sodium alkoxide derivative of the nonionic with a reactive chlorine compound such as the following:
• the terpenyl ethers of the present invention are somewhat more difiicult to produce directly in a substantially fully terminated form,.but as the impurities (unterminated products) are generally no more than 10%, there is no problem in eliminating them by conventional purification techniques so as to leave only the substantially etherified products.
• R a hydrocarbon radical selected from the group consisting of (1) straight and branched chain C -C alkyl radicals, (2) straight and branched chain (I -C al kenyl radicals, and (3) mono and dialkylphenyl radicals containing 10 to 24 carbon atoms;
• R' a hydrocarbon radical selected from the group consisting of (1) tertiary C -C alkyl groups; (2) and alicyclic radicals of the formula C H derived from monoterpenes, in particular for the C1OH17 radical (believed to be isobornyl) which is derived from camphene.
• compositions are those in which: R is p-t-octylphenyl, p-nonylphenyl, p-dodecylphenyl, n-dodecyl, n-
• Examples 1-3 show reactions of a gaseous olefin with a liquid alcohol, a gaseous olefin with a solid alcohol, and a nonvolatile olefin with a liquid alcohol.
• the catalyst employed is Amberlyst 15, a macroreticular structured sulfonated styrene-divinylbenzene copolymer in the dehydrated acid form. This catalyst, a product of the Rohm & Haas Company, Philadelphia, Pennsylvania, is more fully disclosed in Belgian Patent 590,370, which is herein incorporated by reference.
• EXAMPLE 1 Into the bottom portion of a Z-liter-Parr stirring autoclave (stainless steel) charge 453.4 g. (0.5 mol.) of a reaction product of octylphenol and 16 moles of ethylene oxide, and 35 g. of Amberlyst 15 which had previously been dried for 16 hours at 70 C. under an absolute pressure of 0.5 mm. Place the head of the autoclave in place and seal the autoclave. After sealing the autoclave, connect the autoclave to the vacuum source and reduce pressure to -20 mm. on the autoclave. Place the autoclave in the heating jacket and connect the stirrer to the stirring motor. While stirring rapidly charge 326 g.
• isobutylene either as a gas, by connecting the autoclave directly to the isobutylene cylinder (takes about four hours), or as a liquid, by charging the desired amount of liquid isobutylene to a small (one lite-r) breathing oxygen type cylinder and then transferring this liquid isob-utylene to the evacuated autoclave. After transfer of the isobutylene stir the autoclave at room temperatu-re for 18-20 hours. (The pressure will be maintained at 25-30 p.s.i.g. during this time.) At the end of this holding period vent the autoclave through a .tared Dry Ice-trap to collect the unreacted isobutylene to atmosphenic pressure.
• EXAMPLE 2 In a suitable container (.two liter beaker) dissolve 637 g. (0.4 mol.) stearyl-E in 300 ml. of dry dioxane (dried over anhydrous MgSO with heating and stirring. When the stearyl E is completely dissolved transfer this warm (ca. 30-35 C.) solution to the bottom portion of a Parr stirning autoclave (two liter capacity) and then add 100 g. of dry Amber-lyst 15 and seal and evacuate the autoclave as in Example 1.
• EXAMPLE 3 In a one-liter three-necked flask equipped with a mechanical stirrer, a thermometer and a reflux condenser place 228.7 g. (0.153 mol.) dodecylphenol-E 35 g. dry Amberlyst 15 (dried as in Example 1), and 282.5 g. (2.0 mols.) camphene. Heat this mixture at 50-55 C. with stirring for 72 hours. At the end of this time, cool the mixture to room temperature, filter to remove the beads, dilute the filtrate with isopropanol and neutralize the mixture to 7-8 by the addition of alcoholic NaOH.
• a key to the unique method and composition of the present invention resides in the use of the proper catalyst.
• the conventional homogeneous acid catalysts such as p-toluene sulfonic acid, give much slower reaction rates, even When very large amounts of catalyst are used.
• Table I illustrates the superiority of the macroreticular resin catalysts in catalyzing two typical etherification reactions. It is to be noted that the reaction of isobutylene with OPE (the reaction product of octylphenol and 16 moles of ethylene oxide) was substantially complete when the macroreticular resin was used. By contrast the product obtained when the homogeneous catalyst was employed was so poor that it could be put to commercial use only after an expensive purification procedure to remove large amounts of unreacted starting material. Likewise, the reaction of camphene with OPE (the reaction product of octylphenol and 35 moles of ethylene oxide) occurred only to a minor extent when the homogeneous catalyst was used. By comparison, the same reaction was complete when the macroreticular catalyst was used.
• OPE the reaction product of octylphenol and 16 moles of ethylene oxide
• the amount of catalyst needed may vary with the olefins or the alcohols used, and the particular conditions of a given reaction. It should be sufficient to catalyze the reaction, of course, and there is no concern with regard to the possibility of an excess being used. An excess cannot harm the reaction, and since the catalyst is an insoluble material which can be re-used a number of times, there is no economic problem regarding possible waste of the material.
• Patents 2,480,940 and 2,561,254 which disclose the use of nonmacroreticular structured sulfonated ion exchange resin catalysts in reactions of olefins and alcohols, the higher alcohols (above C5-6) reacted only sluggishly, if at all.
• Table II compares the reactions of a number of different alcohols with isobutylene
• Table III compares the reactions of a number of different alcohols with camphene, to show how well the method of the present invention operates, in every case using Amberlyst 15 as the catalyst.
• OPE is the abbreviation for octylphenoxyethanol, and such designations as E or E0 identify the number of oxyethylene units present.
• Vairous conditions for the reactions have been studied.
• pressure atmospheric conditions are suitable in reactions of olefins, having boiling points above 2530.
• a suitable pressure vessel is required, and pressures on the order of 1030 p.s.i.g. may suitably be employed.
• the principal requirement is to have enough pressure to keep an excess of the olefin dissolved in the alcohol.
• reactions using low boiling olefins such as isobutylene are best carried out at about 2027 C. Higher temperatures make the reaction go faster, but temperatures much above 50 C. should be avoided as they give rise to dimerization of the olefin.
• the reactions using camphene are best carried out at about 5060 C. Lower temperatures undesirably slow down the reaction, and higher temperatures in the neighborhood of 100 C. may adversely affect the catalyst.
• a Hamilton-Beach electrically driven mixing apparatus is inserted into a glass tube which is sealed at its bottom end.
• the glass tube is immersed in a Water bath which maintains the temperature within 0.5 C. of the particular test temperature.
• the mixer blades are centered in the tube with the upper blade /2 inch above the solution surface.
• the 200 ml. of 0.1% test solution is equilibrated to temperature and then mixed at high speed (14,500 r.p.m.) for three minutes.
• the mixer is stopped and the foam height recorded after five seconds. A foam height of less than 5.5 cm. is considered acceptable, and anything over that value is deemed unacceptable.
• Each test usually is run in duplicate.
• the food soil defoaming test is performed with a dishwasher, such as the commercially well-known Kitchen Aid apparatus, in which the speed of the rotor is a function of the quantity and character of foam. Foam pumped into the rotor imparts less momentum to the rotor upon leaving than would water without air and hence the rotor moves more slowly.
• EXAMPLE 4 Into a two-liter stainless steel, stirred autoclave were charged 626 parts (1.0 mol) of a reaction product of dodecanol-l and 10 mols of ethylene oxide, the average composition of which can be expressed by the formula I1-C12H25 OCH2CH2)1QOH, parts of Amberlyst 15, which had been dried previously for 16 hours at an absolute pressure of 0.5 mm., and 627 grams (11.2 mols) of liquid isobutylene. The autoclave was closed and the contents stirred at 30 to 38 C. for 22 hours. At the end of this time, the autoclave was opened and the excess isobutylene was allowed to boil off. The contents of the autoclave were then filtered to separate the product from the catalyst beads.
• the beads were washed once with 200 ml. of isopropyl alcohol, which was combined with the filtered product.
• the product solution was neutralized to pH 7 with a little dilute sodium hydroxide solution and was then stripped at 15 mm. pressure and 100 C.
• Six hundred eighty parts of light amber oil were obtained.
• the oil had a hydroxyl number of 4, a cloud point at 1% in water of 42 C. and showed no discoloration when 2 parts were mixed with 98 parts of powdered sodium hydroxide and placed in a closed jar for three weeks.
• the starting material the reaction product of dodecanol-l and 10 mols of ethylene oxide, had a cloud point at 1% in water of 93 C., a hydroxyl number of 90 and turned dark brown in the alkali-stability test.
• EXAMPLE 5 Into a two-liter stainless steel autoclave were charged 596 parts (0.25 mol) of a reaction product of mols of ethylene oxide with dodecanol-l, 300 parts of anhydrous dioxane, 100 parts of dry Amberlyst 15, and 168 parts (3.0 mols) of isobutylene. After 24 hours stirring at 25-30" C., the product was worked up as described TABLE IV.COMPARISON OF FOAMING AND DEFOAMING PROPERTIES OF OLEFIN-TERMINATED AND NON-TERMINATED SURFACTANIS Unterminated Terminated E0 Adduct Defoaming Group Foam 1 Food Soil 2 Foam l Defoamcm. Rotor cm. ing r.p.m.
• Example 1 The product weighed 610 grams, had a hydroxyl number of 2, and was stable to alkali. It was a waxy material, melting at 45-50 C.
• EXAMPLE 6 In a two-liter beaker containing 300 parts of dry dioxane were dissolved 637 parts (0.4 mol) of a reaction product of a commercial grade of n-octadecyl alcohol (Dytol E46) with 30 mols of ethylene oxide. The warm solution (3035 C.) was poured into a two-liter stirred autoclave. One hundred parts of dried Amberlyst 15 and 307.5 parts (5.48 mols) of liquid isobutylene were added. I he autoclave was stirred at 30-33 C. for 24 hours. During this time, the gauge pressure dropped from 36 lbs/sq. inch to 10 lbs/sq. inch. The autoclave was then vented through a Dry-Ice trap to recover the unreacted isobutylene. The product was worked up as in Example 1, giving 615 grams of an amber oil which, on
• Example 1 The contents of the flask were worked up as in Example 1. A practically quantitative yield of 700 grams of product was obtained, having a hydroxyl number of 5. It had a cloud point at 1% of 22 C. and was stable to discoloration on alkali.
• the orginal octylphenol-ethylene oxide reaction product turned dark brown in the alkali stability test. A by-product identified as diisobutylene was obtained in the final stripping of the reaction product.
• EXAMPLE 10 A reaction product of 7 mols of ethylene oxide with octylphenol (514 parts or 1.0 mol of reaction product), 50 g. of dried Amberlyst 15, and 302 grams of isobutylene were agitated 23 hours in an autoclave at 25 C. The product was completely converted to the t-butyl ether and had a cloud point at 1% in water of 1 (2., whereas the starting material had a cloud point of 24 C. The product did not discolor on NaOH or KOl-I, whereas the starting material rapidly turned brown.
• EXAMPLE 16 A mixture of 910 parts of EXAMPLE 17 One hundred grams of the product from Example 16 were mixed with 250 grams of toluene, 250 grams of heptane, 240 grams of isopropyl alcohol and 500 grams of water. After being well agitated the mixture was allowed to separate into layers at 35 C. The upper and lower layers were withdrawn separately and stripped under vacuum to remove solvent. The product from the upper layer, consisting of the purified t-amyl ether, weighed 47 grams. The product from the lower layer, consisting mainly of unreacted octylphenol-E Weighed 50 grams. A comparison of properties of these materials and the crude starting material fiollows.
• EXAMPLE 19 114.2 grams (0.1 mol) of a reaction product of 20 mols of ethylene oxide with dodecylphenol, 125 g. Amberlyst 15, and 168 grams of propylene tetramer (C H 1.0 mol) were heated 48 hours at 5565 C. with agitation.
• the product had a hydroxyl number of 33, compared to a starting hydroxyl number of 49, indicating partial conversion to the ether.
• EXAMPLE 20 In a one-liter, three necked flask equipped with a mechanical stirrer, a thermometer, and a reflux condenser were placed 229 grams (0.153 mol) of dodecylphenol-E grams of dry Amberlyst 15, and 282.5 grams (2.0 mols) of camphene. The mixture was heated with stirring for 72 hours. At the end of this time, the mixture was cooled and filtered to remove the catalyst beads, neutralized to pH 7.5 by addition of 2.0 grams of 10% alcoholic NaOH, and stripped at a final temperature of 100 C. and a pressure of 0.1 mm. The finished product Weighed 236 grams, had a cloud point of 75 C. and a hydroxyl number of 0.5, indicating that it was 99% terminated. The product remained white when mixed with solid NaOH, whereas the starting material rapidly turned brown.
• Example 21 One hundred grams of the product from Example 21 was purified by the procedure of Example 17. Yield was 51 grams of purified alpha-methylbenzyl ether and 41 grams of unreacted octylphenol E A comparison of properties of these materials follows:
• EXAMPLE 23 Five hundred seventy grams (1.0 mol) of an adduct of octanol-2 and 1 0 mols of ethylene oxide was agitated for 10 hours with 280 grams of isobutylene and grams of Amberlyst 15. The product, 2-octyl E -t butyl ether, was separated from the beads, neutralized with a little sodium carbonate and was then stripped to recover excess isobutylene. Six hundred twenty-six grams of a light colored oil 'was obtained. It did not discolor on alkali.
• EXAMPLE 24 A reaction product of iso-octyl alcohol and 10 mols of ethylene oxide was etherified with isobutylene in the manner described in Example 23. The product, iso-octyl- 'E -t-butyl ether. did not discolor on alkali.
• Iso-octyl alcohol is a commercial branched chain 8- carbon primary alcohol prepared by the hydroformylation of mixed heptenes.
• EXAMPLE 25 Four hundred fifty-eight grams (1. 0 mol) of a reaction product of para-t-butylphenol and 7 mols of ethylene oxide was treated with isobutylene as described in Example 10. The product did not discolor on solid NaOI-I.
• EXAMPLE 26 In a one-liter, three necked flask equipped with a thermometer, an agitator, and an inlet for a slow stream of N were heated 131 grams (0.1 mol) of a reaction product of one rnol octylphenol With 25 mols of ethylene oxide, 250 grams of Amberlyst 15 and 136 grams (11 mols) of camphene. After 72 hours at 6570 C. the product was separated from the catalyst beads. The beads were washed once with alcohol to remove additional product.
• the product was an amber oil which solidified at room tem- EXAMPLE 27
• a reaction product of octadecanol-l with 35 mols of ethylene oxide was converted to the isobornyl ether by the method described in Example 26.
• the product had a hydroxyl number of 3.2 and contained about 11 percent by weight of unetherified starting material. It discolored slightly on NaOH.
• EXAMPLE 28 A reaction product of octylphenol and 16 mols of ethylene oxide (91.0 grams) was heated with 136 grams of apinene in the presence of 13 grams of Amberlyst 15 for 48 hours at 3040 C. At the end of this time the prodnot was separated from the catalyst beads, neutralized to pH 7.0, and stripped to remove unreacted u-pinene. Analysis of the stripped product indicated that it was 39% terpenyl ether of OPE and 61% unreacted OPE EXAMPLE 29 Treatment of OPE with di-limonene in the same manner as in Example 28 gave a product containing by analysis 27% of a terpenyl ether of OPE and 73% unreacted oPE We claim:
• the process comprising mixing together a compound having the formula RO(CI-I CH O) OH with a tertiary olefin hydrocarbon having from four to twelve carbon atoms, the ratio of the two being at least two moles of the olefin per mole of alcohol, contacting the mixture with an anhydrous macro-reticular resinous polysulfonic acid at a temperature ranging from about to 70 C.
• R in the formula being a hydrocarbon radical selected from the group consisting of (1) straight and branched chain G -C alkyl radicals, and (2) straight and branched alkenyl radicals, and (3) mono and dialkylphenyl radicals containing to 24 carbon atoms, and the x in the formula being a number from 7 to 50, inclusive.

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  • NL NL288287D patent/NL288287A/xx unknown
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• 1962
  • 1962-02-06 US US171363A patent/US3281475A/en not_active Expired - Lifetime
• 1963
  • 1963-01-23 GB GB2877/63A patent/GB1012821A/en not_active Expired
  • 1963-01-26 DE DE19631520647 patent/DE1520647B2/de active Pending
  • 1963-02-01 SE SE1120/63A patent/SE306177B/xx unknown
  • 1963-02-06 CH CH146463A patent/CH424743A/fr unknown

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